GB1013509A - Process for the purification of pyrolysis gases - Google Patents
Process for the purification of pyrolysis gasesInfo
- Publication number
- GB1013509A GB1013509A GB5048463A GB5048463A GB1013509A GB 1013509 A GB1013509 A GB 1013509A GB 5048463 A GB5048463 A GB 5048463A GB 5048463 A GB5048463 A GB 5048463A GB 1013509 A GB1013509 A GB 1013509A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- zone
- gases
- water
- recycled
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
- C10G5/04—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas with liquid absorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/10—Conditioning the gas to be cleaned
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/11—Purification; Separation; Use of additives by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- General Chemical & Material Sciences (AREA)
- Industrial Gases (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<FORM:1013509/C4-C5/1> A process for removing carbon dust, tar and hydrocarbons containing 8 or more carbon atoms per molecule from pyrolysis gases comprises simultaneously scrubbing and partially cooling by quenching the gases with a relatively hot hydrocarbon oil (e.g. at 100 DEG to 150 DEG C.) in a first zone 5, and completing the cooling by scrubbing with water under highly turbulent flow conditions (to prevent mist formation) in a second zone 17. Condensed oil (at 24) and dust (at 23) are separated, at 21, from the water (at 22), and a major portion of the condensed oil is recycled (via 24 . . . 26) to the zone 5, and a minor portion of the oil is discharged (at 27) for recovery of cyclic hydrocarbons, e.g. xylene, styrene, indene, and naphthalene, contained therein. The scrubbing oil may be a petroleum light oil (initial b.p. above 150 DEG C.). Turbulent flow in the zone 17 is achieved by using a perforated plate tower with impact plates over the perforations, whereby gas velocities through the perforations above 5 m./sec. are obtained. Preferably, as shown, the oil is sprayed at 3 into the gases, which, with vaporized and unvaporized oil, enter a distillation column 5 where oil condenses and from which dust-containing oil is discharged at 6 for separation at 7, oil being recycled, after being suitably made up, at 10, via lines 13, 15. The unsaturated component of the heavy hydrocarbons is polymerized to tar and eliminated via line 6, the gases leaving the column via line 16 containing vaporized oil and mainly cyclic hydrocarbons. In a modification, Fig. 3 (not shown), a heat-exchanger is inserted in the line 16 and condensate (water and oil) removed from the exchanger, separated, a major part of the oil recycled to the top of the column 5, and a minor part discharged for recovery of cyclics. Further, fresh oil is delivered to the top of the scrubber 17 to remove cyclic hydrocarbons, the oil being separated from the water at 21, as before, and part at least delivered via line 26 directly to the line 13. Two examples are described.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP113263 | 1963-01-11 | ||
JP1463963 | 1963-03-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1013509A true GB1013509A (en) | 1965-12-15 |
Family
ID=26334300
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5048463A Expired GB1013509A (en) | 1963-01-11 | 1963-12-20 | Process for the purification of pyrolysis gases |
Country Status (2)
Country | Link |
---|---|
CH (1) | CH409898A (en) |
GB (1) | GB1013509A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4126431A (en) * | 1975-12-05 | 1978-11-21 | Didier Engineering Gmbh | Method for the preliminary treatment of crude gas from a thermic carbon refinement process |
WO2012020221A1 (en) | 2010-08-11 | 2012-02-16 | Novacta Biosystems Limited | Compounds |
CN108384583A (en) * | 2018-03-14 | 2018-08-10 | 深圳市水务(集团)有限公司 | A kind of purification of solid waste pyrolysis gas and the system of utilizing |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU1800083A (en) * | 1982-08-18 | 1984-09-27 | Allis-Chalmers Corp. | Condensing particles from gas using a fraction of the condensate as the primary coolant |
-
1963
- 1963-12-20 GB GB5048463A patent/GB1013509A/en not_active Expired
- 1963-12-30 CH CH1602163A patent/CH409898A/en unknown
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4126431A (en) * | 1975-12-05 | 1978-11-21 | Didier Engineering Gmbh | Method for the preliminary treatment of crude gas from a thermic carbon refinement process |
WO2012020221A1 (en) | 2010-08-11 | 2012-02-16 | Novacta Biosystems Limited | Compounds |
CN108384583A (en) * | 2018-03-14 | 2018-08-10 | 深圳市水务(集团)有限公司 | A kind of purification of solid waste pyrolysis gas and the system of utilizing |
CN108384583B (en) * | 2018-03-14 | 2024-04-02 | 深圳市水务(集团)有限公司 | System for purifying and utilizing pyrolysis gas of solid waste |
Also Published As
Publication number | Publication date |
---|---|
CH409898A (en) | 1966-03-31 |
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